CN101153618A - Connecting structure of liquid feeding device, fuel cell power generation device, and electronic equipment - Google Patents
Connecting structure of liquid feeding device, fuel cell power generation device, and electronic equipment Download PDFInfo
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Images
Classifications
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04082—Arrangements for control of reactant parameters, e.g. pressure or concentration
- H01M8/04201—Reactant storage and supply, e.g. means for feeding, pipes
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
- F04B17/00—Pumps characterised by combination with, or adaptation to, specific driving engines or motors
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
- F04B19/00—Machines or pumps having pertinent characteristics not provided for in, or of interest apart from, groups F04B1/00 - F04B17/00
- F04B19/006—Micropumps
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04082—Arrangements for control of reactant parameters, e.g. pressure or concentration
- H01M8/04201—Reactant storage and supply, e.g. means for feeding, pipes
- H01M8/04208—Cartridges, cryogenic media or cryogenic reservoirs
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/06—Combination of fuel cells with means for production of reactants or for treatment of residues
- H01M8/0606—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants
- H01M8/0612—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants from carbon-containing material
- H01M8/0618—Reforming processes, e.g. autothermal, partial oxidation or steam reforming
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T137/00—Fluid handling
- Y10T137/8593—Systems
- Y10T137/85978—With pump
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- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Manufacturing & Machinery (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Fuel Cell (AREA)
- Reciprocating Pumps (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Degasification And Air Bubble Elimination (AREA)
Abstract
本发明的送液装置的连接构造体,包括:电渗流泵,电极设置在电渗材的上游侧和下游侧;流路构造体,在上述电渗流泵的上游侧和下游侧形成液体的流路,在上述电渗流泵的上游部设有与流路的内外相通的脱气孔,并且,在该脱气孔中设有使气泡通过的疏水性膜;以及吸液体,设在上述电渗流泵的上游侧的送液流路中,与设置上述电渗材的上游侧电极的面抵接而吸收液体,形成有从与上述电极的抵接面侧通到上述疏水性膜侧的气泡除去路径。
The connection structure of the liquid delivery device of the present invention includes: an electroosmotic flow pump, the electrodes are arranged on the upstream side and the downstream side of the electroosmotic material; Road, the upstream part of the above-mentioned electroosmotic flow pump is provided with a degassing hole communicating with the inside and outside of the flow path, and a hydrophobic film that allows air bubbles to pass is provided in the degassing hole; In the upstream liquid-feeding channel, the surface of the upstream-side electrode on which the electroosmotic material is provided abuts to absorb liquid, and a bubble removal path is formed that passes from the side of the abutting surface with the above-mentioned electrode to the side of the above-mentioned hydrophobic membrane.
Description
技术领域technical field
本发明涉及具备利用电渗现象的电渗流泵的送液装置的连接构造体、具备该送液装置的连接构造体的燃料电池型发电装置、以及具备该燃料电池型发电装置的电子设备。The present invention relates to a connection structure of a liquid delivery device including an electroosmotic flow pump utilizing an electroosmotic phenomenon, a fuel cell power generation device including the connection structure of the liquid delivery device, and electronic equipment including the fuel cell power generation device.
背景技术Background technique
近年来,燃料电池作为能量转换效率较高的清洁电源受到瞩目,在燃料电池汽车、便携设备、电化住宅等中得到了广泛的应用。In recent years, fuel cells have attracted attention as a clean power source with high energy conversion efficiency, and have been widely used in fuel cell vehicles, portable devices, and electrified houses.
在燃料电池中,作为用于传送燃料或水的动力源使用泵。泵有离心式、容积旋转式、容积往复式等机械动作的泵,但是,例如日本特开2006-22807号公报所公开的那样,提出了不具备机械可动部就能传送液体的电渗流泵。In a fuel cell, a pump is used as a power source for transferring fuel or water. Pumps include mechanically operated pumps such as centrifugal type, volumetric rotary type, and volumetric reciprocating type. However, as disclosed in Japanese Patent Application Laid-Open No. 2006-22807, an electroosmotic flow pump capable of transferring liquid without a mechanical movable part has been proposed. .
电渗流泵是利用电渗现象的泵,如图18所示地构成。如图18所示,电渗流泵具备:被填充在管材504中的电渗材502;配置在电渗材502的上游侧的电极501;配置在下游侧的电极503。电渗材502例如由配置在管材504的流向上的硅石纤维等电介质构成。The electroosmotic flow pump is a pump utilizing the electroosmotic phenomenon, and is configured as shown in FIG. 18 . As shown in FIG. 18 , the electroosmotic flow pump includes: an
电渗流泵通过以下的原理工作。即,如果液体接触电渗材502的电介质,电介质的表面带电,在该接触界面附近集中液体中的抗衡离子,电荷过剩。在此,若通过在电极501和503之间施加电压使得在电渗材502内产生电场,则液体中的抗衡离子移动,整个液体通过液体的粘性流动。此外,在电渗材502为硅石的情况下,硅石的表面成为Si-O-,硅石的表面带负电,在液体中集中正离子(抗衡离子),在液体中正电荷过剩,所以若将电压施加成使得电极501的电位比电极503的电位高,则流体向如图18所示的方向流动。The electroosmotic pump works by the following principle. That is, when the liquid contacts the dielectric of the electro-
利用上述原理驱动的电渗流泵没有可动部,结构简单,具有能够小型化、无脉动、无噪声等优点。The electroosmotic flow pump driven by the above principle has no movable parts, has a simple structure, and has the advantages of miniaturization, no pulsation, and no noise.
此外,例如日本特愿2006-95958号所示,还提出了在电渗流泵上具备驱动液体的自己充填机构和抽气机构的电渗流泵。In addition, as shown in Japanese Patent Application No. 2006-95958, an electroosmotic flow pump equipped with a self-filling mechanism and an air pumping mechanism for driving liquid is also proposed on the electroosmotic flow pump.
但是,若持续进行电渗流泵的送液,则在两电极上因液体的电分解而产生气泡。因此,在上游侧的电极附近产生的气泡蓄积在电渗流泵的上游侧,所以存在电渗材的有效流路面积变小、液体的送液效率降低的可能性。此外,由于在下游侧的电极附近产生的气泡与液体一起流向下游,所以设在下游的流量传感器有可能因气泡的通过而不能检测出液体的准确流量。However, if the electroosmotic flow pump continues to send liquid, air bubbles are generated on both electrodes due to electrolysis of the liquid. Therefore, air bubbles generated in the vicinity of the upstream electrodes are accumulated on the upstream side of the electroosmotic flow pump, so that the effective flow path area of the electroosmotic material may be reduced and the liquid delivery efficiency of the liquid may be reduced. In addition, since the air bubbles generated near the electrodes on the downstream side flow downstream together with the liquid, the flow sensor installed downstream may not be able to detect the accurate flow rate of the liquid due to the passing of the air bubbles.
发明内容Contents of the invention
本发明提供一种能够良好地除去由电渗流泵的电极产生的气泡的小型送液装置的连接构造体、使用了该送液装置的连接构造体的燃料电池型发电装置以及具备该燃料电池型发电装置的电子设备。The present invention provides a connection structure of a small-sized liquid delivery device that can well remove air bubbles generated by electrodes of an electroosmotic flow pump, a fuel cell power generation device using the connection structure of the liquid delivery device, and a fuel cell power generation device equipped with the fuel cell power generation device. Electronic equipment for power generating units.
根据本发明的一个较佳方式,提供一种送液装置的连接构造体,其包括:电渗流泵,电极设置在电渗材的上游侧和下游侧;流路构造体,在上述电渗流泵的上游侧和下游侧形成液体的流路,在上述电渗流泵的上游部设有与流路的内外相通的脱气孔,并且,在该脱气孔中设有使气泡通过的疏水性膜;以及吸液体,设在上述电渗流泵的上游侧的送液流路中,与设置上述电渗材的上游侧电极的面抵接而吸收液体,形成有从与上述电极的抵接面侧通到上述疏水性膜侧的气泡除去路径。According to a preferred mode of the present invention, a connection structure of a liquid delivery device is provided, which includes: an electroosmotic flow pump, the electrodes are arranged on the upstream side and the downstream side of the electroosmotic material; The upstream side and the downstream side of the above-mentioned electroosmotic flow pump form a liquid flow path, and a degassing hole communicating with the inside and outside of the flow path is provided on the upstream part of the above-mentioned electroosmotic flow pump, and a hydrophobic membrane that allows air bubbles to pass is provided in the degassing hole; and Liquid absorption, provided in the liquid delivery channel on the upstream side of the above-mentioned electroosmotic flow pump, abutting against the surface of the upstream side electrode on which the above-mentioned electroosmotic material is provided to absorb liquid, forming a channel from the contacting surface side of the above-mentioned electrode to the Air bubble removal path on the hydrophobic membrane side.
根据本发明的另一较佳方式,提供一种送液装置的连接构造体,其包括:电渗流泵,电极设置在电渗材的上游侧和下游侧;以及流路构造体,在上述电渗流泵的上游侧和下游侧形成液体的流路,在上述电渗流泵的下游部设置与流路的内外相通的脱气孔,并且,在该脱气孔中设有使气泡通过的疏水性膜;在上述电渗流泵的下游侧的送液流路中,环状地设置上述疏水性膜,在与上述疏水性膜同一平面内的中央配置有流路,该流路中设有使液体透过的亲水性膜。According to another preferred mode of the present invention, a connection structure of a liquid delivery device is provided, which includes: an electroosmotic flow pump, the electrodes are arranged on the upstream side and the downstream side of the electroosmotic material; The upstream side and the downstream side of the osmotic flow pump form a liquid flow path, and a degassing hole communicating with the inside and outside of the flow path is provided on the downstream part of the above-mentioned electroosmotic flow pump, and a hydrophobic membrane that allows air bubbles to pass is provided in the degassing hole; In the liquid-feeding channel on the downstream side of the above-mentioned electroosmotic flow pump, the above-mentioned hydrophobic membrane is arranged annularly, and a flow channel is arranged in the center of the same plane as the above-mentioned hydrophobic membrane. hydrophilic membrane.
根据本发明的又一较佳方式,提供一种送液装置的连接构造体,其包括:电渗流泵,电极设置在电渗材的上游侧和下游侧;以及流路构造体,在上述电渗流泵的上游侧和下游侧形成液体的流路,在上述电渗流泵的上游部或下游部设置与流路的内外相通的脱气孔,并且,在该脱气孔中设有使气泡通过的疏水性膜,在外面设有成为与上述脱气孔相通的气泡除去路径的沟槽。According to yet another preferred mode of the present invention, there is provided a connection structure of a liquid delivery device, which includes: an electroosmotic flow pump, the electrodes are arranged on the upstream side and the downstream side of the electroosmotic material; The upstream side and the downstream side of the osmotic flow pump form a liquid flow path, and a degassing hole communicating with the inside and outside of the flow path is provided on the upstream or downstream portion of the above-mentioned electroosmotic flow pump, and a hydrophobic hole that allows air bubbles to pass is provided in the degassing hole. The membrane is provided with grooves on the outside to serve as air bubble removal paths communicating with the above-mentioned degassing holes.
附图说明Description of drawings
本发明的上述的以及进一步的目的、特征及优点,将会从所附的附图和下面的详细说明变得清楚,但这仅仅是用于说明的,而非限定本发明的范围。The above and further objects, features and advantages of the present invention will become clear from the attached drawings and the following detailed description, but these are only for illustration, not limiting the scope of the present invention.
图1是电子设备1000的框图。FIG. 1 is a block diagram of an electronic device 1000 .
图2是燃料电池型发电装置1的框图。FIG. 2 is a block diagram of the fuel
图3是从燃料盒2侧看送液装置的连接构造体40的立体图。FIG. 3 is a perspective view of the
图4是从流路控制部60侧看送液装置的连接构造体40的立体图。FIG. 4 is a perspective view of the
图5是从燃料盒2侧看送液装置的连接构造体40的分解立体图。FIG. 5 is an exploded perspective view of the
图6是从流路控制部60侧看送液装置的连接构造体40的分解立体图。FIG. 6 is an exploded perspective view of the
图7是图3的沿VII-VII线的剖视图。FIG. 7 is a cross-sectional view along line VII-VII of FIG. 3 .
图8是电渗流泵50的分解立体图。FIG. 8 is an exploded perspective view of the
图9是从燃料盒2侧看第1吸液体41的立体图。FIG. 9 is a perspective view of the first
图10是从流路控制部60侧看第1吸液体41的立体图。FIG. 10 is a perspective view of the first
图11是表示从对应于图5的燃料盒2侧看的气泡的移动路径的图。FIG. 11 is a diagram showing the moving path of air bubbles viewed from the
图12是表示从对应于图6的流路控制部60侧看的气泡的移动路径的图。FIG. 12 is a diagram showing a movement path of air bubbles viewed from the flow
图13是表示对应于图7的气泡的移动路径的图。FIG. 13 is a diagram showing a movement path of air bubbles corresponding to FIG. 7 .
图14是从燃料盒2侧看第1吸液体41的变形例的立体图。FIG. 14 is a perspective view of a modified example of the first absorbing
图15是从流路控制部60侧看第1吸液体41的变形例的立体图。FIG. 15 is a perspective view of a modified example of the first
图16是表示第2吸液体42的变形例的立体图。FIG. 16 is a perspective view showing a modified example of the second
图17是表示第2吸液体42的变形例的立体图。FIG. 17 is a perspective view showing a modified example of the second
图18是用于说明电渗流泵50的原理的图。FIG. 18 is a diagram for explaining the principle of the
具体实施方式Detailed ways
下面,利用附图说明用于实施本发明的最佳方式。在下面所述的实施方式中,虽然为实施本发明而附加了各种技术上的限定,但不是将本发明的范围限定在下面的实施方式及图示例中。Next, the best mode for carrying out the present invention will be described with reference to the drawings. In the embodiments described below, various technical limitations are added for carrying out the present invention, but the scope of the present invention is not limited to the following embodiments and illustrated examples.
【电子设备】【Electronic equipment】
图1是电子设备1000的框图。电子设备1000具备:燃料电池型发电装置1;将由燃料电池型发电装置1生成的电能变换成适当的电压的DC/DC转换器904;与DC/DC转换器904连接的2次电池905;控制燃料电池型发电装置1、DC/DC转换器904和2次电池905的控制部906;以及由DC/DC转换器904供给电能的电子设备主体901。FIG. 1 is a block diagram of an electronic device 1000 . The electronic device 1000 includes: a fuel cell type
燃料电池型发电装置1如后所述,生成电能并输出到DC/DC转换器904。DC/DC转换器904除了具备将由燃料电池型发电装置1生成的电能转换为适当的电压之后、向电子设备主体901或控制部906供给的功能之外,还具备以下功能:将由燃料电池型发电装置1产生的电能向2次电池905充电,在燃料电池型发电装置1不工作时,将蓄积在2次电池905中的电能供给电子设备主体901或控制部906。控制部906控制燃料电池型发电装置1或DC/DC转换器904,以便向电子设备主体901稳定地供给电能。The fuel
下面,详细说明燃料电池型发电装置1。Next, the fuel
【燃料电池型发电装置】【Fuel cell power generation device】
图2是燃料电池型发电装置1的框图。燃料电池型发电装置1包括:燃料盒2、2;送液装置的连接构造体40、40;流路控制部60;微反应器6及发电单元20(燃料电池装置);以及气泵30等。燃料电池型发电装置1是具备两个燃料盒2、2的系统。FIG. 2 is a block diagram of the fuel
流路控制部60例如由层叠了多片基板的多层基板构成,在流路控制部60上,面安装了送液装置的连接构造体40、40、微反应器6、发电单元20、气泵30。此外,流路控制部60具备微阀33~35和流量传感器36~38(内置)。The flow
微阀33是通过关闭和打开来允许或阻止从送液装置的连接构造体40、40向气化器7流入的混合液的流动的开关阀。微阀34是控制从气泵30流向微反应器6内的一氧化碳清除器9中的空气流量的控制阀(可调阀)。微阀35是控制从气泵30流向微反应器6内的燃烧器10中的空气流量的控制阀(可调阀)。The
流量传感器36设在从燃料盒2、2到微反应器6内的气化器7的流路中,检测从燃料盒2、2流向气化器7的混合液的流量。流量传感器37设在从气泵30到微反应器6内的一氧化碳除去器9的流路中,检测从气泵30流向一氧化碳清除器9的空气流量。流量传感器38设在从气泵30到微反应器6内的燃烧器10的流路中,检测从气泵30流入微反应器6内的燃烧器10的空气流量。The
燃料盒2内贮留着燃料和水的混合液。在燃料盒2、2的壁面上形成有燃料排出孔。在燃料排出孔中,嵌入了止回阀。在止回阀上插入了后述的送液装置的连接构造体40的吸液体41。A mixture of fuel and water is stored in the
该止回阀是将具有可挠性和弹性的材料(例如弹性体)形成为鸭嘴状的鸭嘴阀,将该鸭嘴状的前端以朝向燃料盒2、2的内部的状态嵌入。通过止回阀,能够防止混合液从燃料排出孔向燃料盒2的外部泄露。The check valve is a duckbill valve formed of a flexible and elastic material (for example, elastomer) into a duckbill shape, and the duckbill-shaped tip is inserted so as to face the inside of the
燃料排出孔被设置成与送液装置的连接构造体40、40对置,燃料盒2、2能够安装在送液装置的连接构造体40、40上或从其拆下。The fuel discharge hole is provided to face the
送液装置的连接构造体40、40分别具备吸液体41、42以及电渗流泵50。第1吸液体41具有吸液性,插入到燃料排出孔的止回阀上,吸收燃料盒2、2内的混合液。第2吸液体42由比第1吸液体41软的纤维材料构成,吸收由第1吸液体41吸收的混合液。The
电渗流泵50如后所述地吸收由第2吸液体42吸收的混合液,送到微反应器6内的气化器7。The
如图2所示,微反应器6是将气化器7、改质器8、一氧化碳除去器9和燃烧器10单元化的机构,气化器7与改质器8相通,改质器8与一氧化碳除去器9相通。微反应器6被收容在真空隔热封装11中。As shown in Figure 2, the
在微反应器6的与流路控制部60相对置的面上,设有6个端口12~17。微反应器第1端口12是与气化器7相通的输入端口,微反应器第2端口13是与一氧化碳除去器9相通的输入端口;微反应器第3端口14是与燃烧器10相通的输入端口;微反应器第4端口15是来自燃烧器10的输出端口;微反应器第5端口16是与燃烧器10相通的输入端口;微反应器第6端口17是来自一氧化碳清除器9的输出端口。Six
发电单元20是将具有触媒的燃料极21、具有触媒的氧气极22、被夹持在燃料极21和氧气极22之间的电介质膜23单元化的构件。The
在发电单元20的与流路控制部60相对置的面上,设置了4个端口24~27。发电单元第1端口24是与燃料极21相通的输入端口,发电单元第2端口25是来自燃料极21的输出端口,发电单元第3端口26是与氧气极22相通的输入端口,发电单元第4端口27是来自氧气极27的输出端口。Four
如图2所示,在气泵30的吸引侧设有空气过滤器31,外部空气通过空气过滤器31被吸引到气泵30中。在气泵30设有排出端口32,被吸引到气泵30中的空气从排出端口32排出,通过流路控制部60内的流路,供给到各部。As shown in FIG. 2 , an
【燃料电池型发电装置的工作】【Operation of Fuel Cell Power Plant】
接着,说明该燃料电池型发电装置1的工作。Next, the operation of the fuel
首先,通过送液装置的连接构造体40、40的作用,从燃料盒2向气化器7输送混合液。First, the liquid mixture is sent from the
另一方面,若气泵30工作,则外部空气通过空气过滤器31被吸引到气泵30,被吸引的空气从排出端口32送到一氧化碳除去器9、燃烧器10及氧气极22。On the other hand, when the
被送到氧化器7的混合液被气化,气化的燃料和水的混合气被送到改质器8。在改质器8中,利用从气化器7供给的混合气,通过改质反应触媒生成氢气和二氧化碳,还生成微量的一氧化碳。此外,在燃料盒2内的混合液是甲醇和水的混合液的情况下,在改质器8中起如化学反应式(1)、(2)所示的触媒反应。The mixed liquid sent to the
CH3OH+H2O→3H2+CO2......(1) CH3OH + H2O → 3H2 + CO2 ...(1)
H2+CO2→H2O+CO......(2)H 2 +CO 2 →H 2 O+CO...(2)
在改质器8中生成的混合气被供给到一氧化碳除去器9,与从气泵30的排出端口32经由微反应器第2端口13供给的空气混合。在一氧化碳除去器9中,如化学反应式(3)所示,通过选择氧化反应触媒,混合气中的一氧化碳气体被优先氧化(燃烧),除去了一氧化碳。The mixed gas generated in the reformer 8 is supplied to the
2CO+O2→2CO2(3)2CO+O 2 →2CO 2 (3)
在被除去了一氧化碳的状态的混合气中含有氢气,该混合气从微反应器第6端口17经由发电单元第1端口24,被供给到发电单元20的燃料极21。从气泵30的排出端口32经由发电单元第3端口26向氧气极22供给空气。此外,从微反应器第6端口17经由发电单元第1端口24供给到燃料极21的混合气中的氢气,通过电介质膜23与被供给到氧气极22的空气中的氧气进行电化学反应,由此在燃料极21和氧气极22之间产生电力。Hydrogen is contained in the mixed gas in the state from which carbon monoxide has been removed, and the mixed gas is supplied to the
此外,在电介质膜23是氢离子透过型的电介质膜(例如,固体高分子电介质膜)的情况下,在燃料极21中产生下面的式(4)所示的反应,在燃料极21生成的氢离子透过电介质膜23,在氧气极22产生下面的式In addition, when the
(5)所示的反应。The reaction shown in (5).
H2→2H++2e-......(4)H 2 →2H + +2e - ......(4)
2H+1/2O2+2e→H2O......(5)
在氧气极22未反应的空气,从发电单元第4端口27被排出到外部。包含在燃料极27未反应的氢气的混合气,从作为输出端口的发电单元第2端口25经由微反应器第5端口16被输送到燃烧器10。再者,从气泵30的排出端口32经由微反应器第3端口14向燃烧器10供给空气。此外,在燃烧器10内,通过使氢气氧化而产生燃烧热,利用该燃烧热,气化器7、改质器8和一氧化碳除去器9被加热。此外,包含各种生成物的混合气从燃烧器10的输出端口即微反应器第4端口被排出到外部。Unreacted air in the
【送液装置的连接构造体】[Connection structure of liquid feeding device]
在此,对送液装置的连接构造体40的详细结构进行说明。图3是从燃料盒2侧看送液装置的连接构造体40的立体图,图4是从流路控制部60侧看送液装置的连接构造体40的立体图,图5是从燃料盒2侧看送液装置的连接构造体40的分解立体图,图6是从流路控制部60侧看送液装置的连接构造体40的分解立体图,图7是图3的沿VII-VII线的剖视图。Here, the detailed structure of the
如图3~图7所示,送液装置的连接构造体40是接合电渗流泵50、第1吸液体41、第2吸液体42、外壳43、入口侧流路构造体44和出口侧流路构造体45等构成的。As shown in FIGS. 3 to 7, the
图8是电渗流泵50的分解立体图。电渗流泵50包括电渗材51、保持构件52、引出电极53、54。FIG. 8 is an exploded perspective view of the
电渗材51在保持构件52内贴紧侧面而收容。由保持构件52固定电渗材51的径向位置。The
电渗材51是由电介质的多孔材(例如多孔陶瓷等)、纤维材或粒子充填材以圆板状形成,具有吸液性。在电渗材51的两面,通过溅射、蒸镀白金等形成有电极。The
引出电极53、54配置成接触电渗材51两面的电极。在引出电极53、54上,形成有直径比电渗材51还小的圆形开口53a、54a。该电极53、54的内周部与电渗材51的电极的外周部抵接。利用引出电极53、54固定了电渗材51的轴向位置。The
此外,在引出电极53的开口53a的内部,第2吸液体52和电渗材51抵接。电渗材51吸收渗透到第2吸液体42中的混合液。In addition, inside the opening 53 a of the lead-
作为引出电极53、54的材料,可以使用铁、铜合金、SUS等,为了防止与电极及混合液的接触所引起的氧化反应,实施了镀金处理。引出电极和电渗材51的电极面的连接,可以使用具有导电性的粘接剂(例如藤仓化成制ド一タイトFA730,XA-819)进行。As the material of the
图9是从燃料盒2侧看第1吸液体41的立体图,图10是从流路控制部60侧看第1吸液体41的立体图。如图9、图10所示,第1吸液体41是将棒状部41a和圆板部41b一体形成的结构。该第1吸液体41形成为硬质的多孔构造,具有吸液性。第1吸液体41例如由将实施了液体渗透处理的聚乙烯或聚丙稀粒子烧结而构成的多孔体等构成。FIG. 9 is a perspective view of the first
在板状部41b的中央直立设置了棒状部41a,为了保证强度,被收容到外壳43内。外壳43为筒状,例如通过将SUS等金属进行塑性加工、切削加工等形成。在燃料盒2、2被安装在流路控制部60的状态下,棒状部41与外壳43一起插入到燃料排出孔的止回阀中,接触到燃料盒2、2内的混合液。并且,燃料盒2、2内的混合液从棒状部41的前端被吸收到第1吸液体41。The rod-shaped
棒状部41a通过燃料盒2、2的更换,在燃料排出孔的止回阀中反复装卸(插拔),但是由于由外壳43进行加强,所以能够防止棒状部41a反复装卸(插拔)造成的破损。The rod-shaped
圆板部41b的直径大致与第2吸液体42及电渗流泵50的电渗材51相同,通过毛细管力使燃料从多孔体的芯状部向接触面移动,在电渗材51的有效流路面积上,使燃料有效地接触。The diameter of the
如图9、图10所示,在圆板部41b放射状地形成有3个切口41c。As shown in FIGS. 9 and 10 , three
第2吸液体42被夹持配置在第1吸液体41的圆板部41b和电渗材51之间。第2吸液体42具有吸液性,吸收渗透到圆板部41b的混合液。第2吸液体42是将比第1吸液体41更软的纤维材料形成为圆板状的结构,具有可挠性,可弹性变形。因此,能够缓和从第1吸液体41传递到电渗材51的冲击,此外,由于使得第1吸液体41和电渗材51的紧密接触性变好,所以能够将由第1吸液体41吸收的液体有效地送到电渗材51。The second
作为这样的第2吸液体42,能够使用将容易透湿燃料或水且亲水性高的材料或氢氧基结合在内部表面来提高亲水性的材料,例如能够由粘胶丝等无纺布或聚氨酯等海绵、毛毡等形成。As such a second liquid-
在第2吸液体42上,与第1吸液体41的圆板部41b同样,放射状地刻有切口42c。In the second
形成在第1吸液体41及第2吸液体42上的切口41c、42c,成为将从电渗材51表面的电极产生的气泡导向泵外部的气泡除去路径。此外,切口41c、42c的宽度越接近外侧越宽,使得气泡容易逃逸到外侧。The
入口侧流路构造体44相对于电渗流泵50设在燃料盒2侧。入口侧流路构造体44在中央嵌合外壳43,并且具有插通棒状部41a的导入孔44a,导入孔44a的外周部在上下方向上被夹持在外壳43和圆板部41b之间。The inlet-
在入口侧流路构造体44的燃料盒2一侧的面上,在导入孔44a的周围形成环状沟槽44b,从环状沟槽44b向外侧4个方向形成有直线状沟槽44c。在环状沟槽44b上,形成有贯通入口侧流路构造体44的多个脱气孔44d。该环状沟槽44b、直线状沟槽44c及脱气孔44d成为氧气去除路径(气泡除去路径)。On the
即使入口侧流路构造体44的燃料盒2侧的面紧贴燃料盒2的面,也能够通过设置环状沟槽44b、直线状沟槽44c,在不使脱气孔44d堵住的情况下,能够将从脱气孔44d排出的气泡可靠地排出到外部。Even if the surface of the inlet-
在入口侧流路构造体44的电渗流泵50侧的面上,形成有收容圆板部41b的凹部44e。在凹部44e中贯通多个脱气孔44d,并且覆盖脱气孔44d粘贴有环状的疏水性膜44f。疏水性膜44f具有透过氧气或氢气这样的气体,却不透过水、甲醇这样的液体的性质。On the surface of the inlet-
搭载在电子设备上的燃料电池,有时不能固定设备的姿势。尤其是在时常携带使用的笔记本电脑这样的设备中,配置在燃料电池主体内的送液装置也会不分上下方。配置在电渗流泵50上的环状的疏水性膜44f,在电渗流泵50的上下方不确定的情况下,也能够使从电渗材51表面的入口侧的电极产生的气泡不留在泵内,而稳定地排出到外部。A fuel cell mounted on an electronic device may not be able to fix the posture of the device. Especially in devices such as notebook computers that are often carried and used, the liquid delivery device arranged in the main body of the fuel cell will not be distinguished from top to bottom. The ring-shaped
凹部44e的外周部与引出电极53接合,从第1吸液体41及第2吸液体42的切口41c、42c排出的氧气气泡被引导到脱气孔44d。The outer peripheral portion of the
在出口侧流路构造体45中,在流路控制部60侧的一面的中央突出设置有连接管45a,在连接管45a的内部形成有混合液的流路。连接管45a连接到与流路控制部60的微阀33连接的流路上。In the outlet-
在出口侧流路构造体45的流路控制部60侧的一面上,在连接管45a的周围形成有环状沟槽45b,从环状沟槽45b向外侧四个方向形成有直线状沟槽45c。在环状沟槽45b中,形成有贯通出口侧流路构造体45的多个脱气孔45d。该环状沟槽45b、直线状沟槽45c及脱气孔45d成为氢气除去路径(气泡除去路径)。An
即使出口侧流路构造体45的流路控制部60侧的面和流路控制部60的面贴紧,也能够通过设置环状沟槽45b、直线状沟槽45c,使脱气孔45d不堵塞,将从脱气孔45d排出的气泡能够可靠排出到外部。Even if the surface of the outlet-side
在出口侧流路构造体45的电渗流泵50侧的面上,形成有与连接管45a的流路连接的凹部45e,在凹部45e贯通着脱气孔45d。在凹部45e覆盖着脱气孔粘贴有环状的疏水性膜45f,并且覆盖着连接管45a的流路粘贴有亲水性膜45g。亲水性膜45g与疏水性膜44f、45f相反,具有透过水、甲醇这样的液体,不透过氧气或氢气这样的气体的性质。On the surface of the outlet-
在出口侧,也环状地设置有疏水性膜45f,因此,不依赖于设备的姿势,能够将从电渗材51表面的出口侧电极产生的气泡不留在泵内而稳定地排出到外部。Also on the outlet side, the
作为疏水性膜44f、45f例如能够使用“始漏点(break through point)”(在增加内压时液体开始通过膜的压力值)为280kPa的アドバンテツク公司制的T020A,作为亲水性膜45g,可以使用例如最低泡点(bubblepoint)(在增加内压时气泡开始通过膜的压力值)为250kPa的日本Pall公司制的SUPOR-450。As the
(亲水性膜的最低泡点及疏水性膜的最低始漏点分别越高,就越能够防止亲水性膜的气泡漏泄及疏水性膜的液体漏泻,但为了使膜致密,在亲水性膜的液体通过及疏水性膜的气泡通过时会产生压力损失,容易导致泵性能降低。因此,需要设定符合电渗材的性能的亲水性膜及疏水性膜。)(The higher the minimum bubble point of the hydrophilic membrane and the lowest leakage point of the hydrophobic membrane, the more it can prevent the bubble leakage of the hydrophilic membrane and the liquid leakage of the hydrophobic membrane, but in order to make the membrane dense, the hydrophilic When liquid passing through the aqueous membrane and air bubbles passing through the hydrophobic membrane, a pressure loss will occur and the performance of the pump will easily decrease. Therefore, it is necessary to set a hydrophilic membrane and a hydrophobic membrane that match the performance of the electroosmotic material.)
凹部45e的外周部与引出电极54接合,从阴极产生的氢气气泡被引导到脱气孔45d。The outer peripheral portion of the
此外,入口侧流路构造体44、出口侧流路构造体45和引出电极53、54的接合,以及引出电极53、54和保持构建52之间的接合也可以使用粘接剂,只要不脱离本发明的内容,则可以在4个角部设置孔并用螺钉固定等,接合条件和形状可自由变化。In addition, the bonding of the inlet
【送液装置的连接构造体的工作】[Operation of the connection structure of the liquid feeding device]
接着,对送液装置的连接构造体40的工作进行说明。Next, the operation of the
首先,将燃料盒2、2安装在流路控制部60上,若将棒状部41a与外壳43一起插入到燃料排出孔的止回阀中,则棒状部41a与燃料盒2、2内的混合液接触,燃料盒2、2内的混合液从棒状部41a的前端被吸收到第1吸液体41。First, the
此外,被第1吸液体41吸收的混合液浸透到第2吸液体42和电渗材51中。In addition, the liquid mixture absorbed by the
在混合液浸透到电渗材51的状态下,若以与第2吸液体42接触的面的电极成为阳极、相反侧的电极成为阴极的方式,对两个引出电极53、54之间施加电压,则电渗材51内的混合液得到驱动力向阴极侧移动,第2吸液体42内的混合液从阳极侧浸透到电渗材51内。由此,混合液从阳极侧被输送到阴极侧。被输送到阴极侧的混合液透过亲水性膜而流到连接管45a。In the state where the mixed solution permeates the
若继续进行混合液的送液,则通过混合液中的水的电分解,在阳极附近产生氧气气泡,在阴极附近产生氢气气泡。氧气气泡沿着形成于第1吸液体41、第2吸液体42上的切口41c、42c被引导到外侧。这时,切口41c、42c的宽度越靠近外侧越宽,所以小的气泡一边相互结合而变大一边被引导到外侧。If the feeding of the mixed solution is continued, oxygen gas bubbles are generated near the anode and hydrogen gas bubbles are generated near the cathode due to electrolysis of water in the mixed solution. The oxygen bubbles are guided to the outside along the
从切口41c、42c排出的氧气气泡经由入口侧流路构造体44内的凹部44e,并通过疏水性膜44f、脱气孔44d后,从形成在入口侧流路构造体44的外侧的环状沟槽44b及直线状沟槽44c被排出到外部。Oxygen bubbles discharged from the
另一方面,氢气气泡通过混合液从阴极附近流过,经由出口侧流路构造体45内的凹部45e,并通过疏水性膜45f、脱气孔45d,从形成在出口侧流路构造体45外侧的环状沟槽45b及直线状沟槽45c被排出到外部。此外,由于连接管45a的流路被亲水性膜45g覆盖,所以氢气气泡不会流入到连接管45a的流路中。On the other hand, the hydrogen gas bubbles flow through the mixed solution from the vicinity of the cathode, pass through the
为了容易理解气泡的移动路径(除去路径),图11、图12及图13示出将气泡引导到泵外部的除去路径。图11、图12及图13是分别与图5、图6及图7对应的图,在图中用白圈表示气泡,用箭头表示气泡的移动路径。In order to easily understand the movement path (removal path) of air bubbles, FIG. 11 , FIG. 12 , and FIG. 13 show the removal path that guides air bubbles to the outside of the pump. 11 , 12 and 13 are diagrams respectively corresponding to FIG. 5 , FIG. 6 and FIG. 7 , in which bubbles are indicated by white circles and moving paths of the bubbles are indicated by arrows.
此外,在入口侧流路构造体44的燃料盒2侧的面与燃料盒2的面紧贴的情况下,从入口侧的脱气孔44d排出的气泡通过环状沟槽44b、直线状沟槽44c并移动。此外,在出口侧流路构造体45的流路控制部60侧的面和流路控制部60的面紧贴的情况下,从出口侧的脱气孔44d排出的气泡通过环状沟槽45b和直线状沟槽45c并移动。In addition, when the surface of the inlet-
可以理解到,将燃料利用毛细管力从多孔体的芯状部朝向接触面移动的功能、和将从电渗材的电极产生的气泡引导到泵外部的气泡除去路径,通过该构造同时成立。It can be understood that the function of moving the fuel from the core portion of the porous body toward the contact surface by capillary force and the air bubble removal path that guides the air bubbles generated from the electrodes of the electroosmotic material to the outside of the pump are simultaneously established by this structure.
如上所述,根据本实施方式的送液装置的连接构造体40,能够除去由电渗泵50的电极产生的气泡。因此,不会有因在上游侧的电极附近产生的气泡蓄积而发生的电渗材51的有效流路面积变小的现象,能够维持液体的送液效率。此外,由于在下游侧的电极附近产生的气泡不会与液体一起流入到连接管45a的流路中,所以气泡不会通过设在下游的流量传感器36,能够检测出液体准确的流量。As described above, according to the
此外,由于疏水性膜形成为环状,脱气孔配置成环状,所以能够不依赖于送液装置的连结构造体40被配置的方向,能够可靠除去气泡。In addition, since the hydrophobic membrane is formed in a ring shape and the degassing holes are arranged in a ring shape, air bubbles can be reliably removed regardless of the direction in which the
此外,疏水性膜形成为环状,在设有疏水性膜的同一平面内的中央配置有设置了使液体通过的亲水性膜的流路,所以能够使送液装置的连接构造体40的厚度变薄。In addition, the hydrophobic membrane is formed in a ring shape, and the flow channel provided with the hydrophilic membrane that allows the liquid to pass is arranged in the center of the same plane where the hydrophobic membrane is provided, so that the
【第一实施例】【The first embodiment】
在作为疏水性膜使用アドバンテツク公司制的To2oA、作为亲水性膜使用日本ポ一ル公司制的SUPOR-450这样组合时,确认了以下情况:液体通过亲水性膜流到下游侧流路,气泡利用内压通过疏水性膜、脱气孔,从形成在入口侧流路构造体的外侧的氧气除去路径、以及形成在出口侧流路构造体的外侧的氢气除去路径被排出到外部。When To2oA manufactured by Advantec Co., Ltd. was used as the hydrophobic membrane, and SUPOR-450 manufactured by Nippon Ball Co., Ltd. was used as the hydrophilic membrane, it was confirmed that the liquid flowed through the hydrophilic membrane to the downstream channel. Bubbles pass through the hydrophobic membrane and the degassing hole by internal pressure, and are discharged to the outside from the oxygen removal path formed outside the inlet side flow path structure and the hydrogen gas removal path formed outside the outlet side flow path structure.
<第一变形例><First modified example>
此外,在上述实施方式中,如图9、图10所示,在第1吸液体41的圆板部41b设置了3个切口41c,但也可以如图14、图15所示,进一步设置多个(图14、图15中为6个)切口41d,在第2吸液体42上也同样设置切口(未图示),以便更容易排出气泡。In addition, in the above-mentioned embodiment, as shown in FIGS. 9 and 10, three
<第二变形例><Second modification>
此外,如图16所示,也可以在第2吸液体42上放射状地设置多个贯通孔42e,来代替切口42c,从贯通孔42e排出气泡。同样,也可以在第1吸液体41上放射状地设置多个贯通孔(未图示)。In addition, as shown in FIG. 16, a plurality of through-
<第三变形例><Third modification>
此外,如图17所示,也可以在第2吸液体42上设置多个从中心朝向外周方向的曲折形状的切口42f,以代替放射状的切口42c,并从该曲折形状的切口42f排出气泡。此外,也可以在第1吸液体41设置同样的曲折形状的切口(未图示)。In addition, as shown in FIG. 17, instead of the
在此引用和组合了于2006年9月27日提出的日本发明专利申请第2006-263045号的说明书、权利要求、附图和摘要的内容。The contents of the specification, claims, drawings and abstract of Japanese Patent Application No. 2006-263045 filed on September 27, 2006 are incorporated herein by reference and incorporation.
虽然在上面示出说明了各种典型的实施方式,但是本发明并不限于上述实施方式。因此,本发明的范围只是由下面的权利请求范围来限定。Although various typical embodiments have been shown and described above, the present invention is not limited to the above-described embodiments. Accordingly, the scope of the present invention is to be limited only by the scope of the following claims.
Claims (11)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP263045/2006 | 2006-09-27 | ||
| JP2006263045A JP4893195B2 (en) | 2006-09-27 | 2006-09-27 | Liquid feeder connection structure, fuel cell type power generator and electronic device |
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| Publication Number | Publication Date |
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| CN101153618A true CN101153618A (en) | 2008-04-02 |
| CN101153618B CN101153618B (en) | 2010-06-23 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN2007101618995A Expired - Fee Related CN101153618B (en) | 2006-09-27 | 2007-09-27 | Connecting structure of a liquid sending apparatus, fuel-cell type electricity generating apparatus, and electronic device |
Country Status (5)
| Country | Link |
|---|---|
| US (1) | US8038862B2 (en) |
| JP (1) | JP4893195B2 (en) |
| KR (1) | KR100896840B1 (en) |
| CN (1) | CN101153618B (en) |
| TW (1) | TWI350025B (en) |
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| CN104707673A (en) * | 2013-12-15 | 2015-06-17 | 中国科学院大连化学物理研究所 | Electroosmotic pump |
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| JP5082979B2 (en) * | 2008-03-27 | 2012-11-28 | カシオ計算機株式会社 | Control method and control device for electroosmotic pump and fuel cell system |
| US9314567B2 (en) * | 2010-03-09 | 2016-04-19 | Board Of Regents Of The University Of Texas System | Electro-osmotic pumps, systems, methods, and compositions |
| CN116914322B (en) * | 2023-09-13 | 2024-01-09 | 比亚迪股份有限公司 | Cooling system, battery pack case, battery pack, and vehicle |
| CN117844638B (en) * | 2023-12-27 | 2025-05-27 | 深圳摩方新材科技有限公司 | Biological reaction system |
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- 2007-09-27 US US11/862,912 patent/US8038862B2/en not_active Expired - Fee Related
- 2007-09-27 CN CN2007101618995A patent/CN101153618B/en not_active Expired - Fee Related
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN104707673A (en) * | 2013-12-15 | 2015-06-17 | 中国科学院大连化学物理研究所 | Electroosmotic pump |
| WO2015085626A1 (en) * | 2013-12-15 | 2015-06-18 | 中国科学院大连化学物理研究所 | Electroosmotic pump |
| CN104707673B (en) * | 2013-12-15 | 2016-08-17 | 中国科学院大连化学物理研究所 | A kind of electroosmotic pump |
Also Published As
| Publication number | Publication date |
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| TWI350025B (en) | 2011-10-01 |
| TW200822432A (en) | 2008-05-16 |
| KR20080028778A (en) | 2008-04-01 |
| CN101153618B (en) | 2010-06-23 |
| US20080076002A1 (en) | 2008-03-27 |
| KR100896840B1 (en) | 2009-05-12 |
| JP4893195B2 (en) | 2012-03-07 |
| US8038862B2 (en) | 2011-10-18 |
| JP2008082246A (en) | 2008-04-10 |
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